Chlorendic anhydride/maleic anhydride compositions and method for preparing same
a technology of chlorendic anhydride and composition, which is applied in the preparation of carboxylic compounds, organic chemistry, chemistry apparatus and processes, etc., can solve the problems of inability to achieve the final reaction product, the unsatisfactory effect of color and flammability, and the inability to achieve the product form
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example 1
[0041] Eight hundred (800) parts of HCCPD were placed in a glass reactor equipped with heating means, a thermometer, a water-cooled condenser, a mechanically driven stirrer, an addition funnel equipped with means for heating the contents, a gas inlet tube extending to the bottom of the reactor and connected to a compressed air source, and a gas inlet providing a nitrogen atmosphere above the reactants.
[0042] With the gases flowing through both inlets, the HCCPD was heated to 160° C., at which time 373.9 parts of molten maleic anhydride were gradually added from the heated addition funnel. The temperature of the maleic anhydride in the funnel was 90° C. The maleic anhydride was added to the reactor at a rate of 6.2 grams per minute while the contents of the reactor were stirred and heated at 160° C.
[0043] Following completion of the MA addition, stirring and heating of the reaction mixture at 160° C. was continued for about 4 hours together with the flow of gases through both gas i...
example 2
[0045] This example describes 1) an alternative method for preparing the chlorendic anhydride / maleic anhydride mixtures of the present invention and 2) addition of a glycol to form a polyester precursor.
Step 1—Production of Crude Chlorendic Anhydride
[0046] One hundred and fifty (150) parts of HCCPD were placed in a glass reactor equipped with heating means, thermometer, water-cooled condenser, mechanically activated stirrer, a pressure-equalizing addition funnel equipped with a heating means, a gas inlet tube extending to the bottom of the reactor and connected to a compressed air source, and a gas inlet providing a nitrogen atmosphere above the reactants. Using a compressed air flow rate of 9.52 ml. / minute and a nitrogen flow rate of 90.48 ml. / minute the HCCPD was heated to 174° C., at which time 53.92 parts of molten MA were added from the heated addition funnel over a 90 minute period with stirring.
[0047] Heating of the reaction mixture was continued for an additional 30 to 4...
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